TiN基IrO2-Ta2O5涂层析氢电极的催化性能

 采用热分解法制备了以离子镀TiN膜为基体的IrO2-Ta2O5涂层电极,通过循环极化曲线并结合扫描电镜、 X射线能谱和X射线衍射研究了涂层的析氢电催化性能. 结果表明,涂层呈多孔多裂纹的结构,焙烧温度对涂层的表面形貌和电催化活性影响很大. 420 ℃下焙烧的涂层具有最优的电催化活性. 涂层电极的析氢反应电极电位为-0.26 V(vs SCE), 低析氢过电位下的Tafel斜率为-0.04 V, 而在高析氢过电位下,电极表面吸附的大量氢原子改变了氧化物电极的结构,从而抑制了氧的阴极还原反应.     

草酸在Ti/IrO2-Ta2O5阳极圆柱形电解槽中的电催化氧化降解动力学

从电催化氧化降解有机污染物的机理出发,研究了草酸在Ti/IrO2-Ta2O5阳极圆柱形电解槽中的电催化氧化过程,建立了描述整个降解过程的瞬时电流效率与溶液本体有机物浓度的关系式. 通过实验对模型进行了验证,实验结果与模型计算结果基本一致,并讨论了误差产生的原因.     

添加碳纳米管对钌铱锡氧化物阳极性能的影响

本文采用热分解法制备Ti/Ru-Ir-Sn氧化物阳极,运用TGA、SEM、EDS、循环伏安、电化学交流阻抗、极化曲线以及强化电解寿命测试方法,探讨添加不同含量碳纳米管（CNTs）对Ti/Ru-Ir-Sn氧化物阳极的影响规律. 热重分析和阳极能谱数据表明,在烧结温度470 ^oC条件下CNTs未发生高温氧化分解,仍以单质形式存在阳极涂层中. 与对比样品相比,涂层表面裂纹增多,但仍保持典型形貌. 添加CNTs显著改善了Ti/Ru-Ir-Sn氧化物阳极的电化学性能,增大了阳极的活性表面积,减小了涂层内部电阻,提高了阳极析氯电催化活性,析氯电位增加缓慢,阳极强化电解寿命也得到明显延长. 其中,添加0.1 g·L^-1 CNTs的Ti/Ru-Ir-Sn氧化物阳极电催化活性和稳定性最优.     

Ti/RuO2-IrO2-SnO2-Sb2O5阳极在农村饮用水消毒中的应用

采用热分解法制备了一种新型高效析氯阳极Ti/RuO₂-IrO₂-SnO₂-Sb₂O₅,将其应用于农村饮用水消毒频繁停开、低电解液浓度的特殊工况下,并与Ti/RuO₂-SnO₂-Sb₂O₅、Ti/RuO₂-TiO₂、Ti/RuO₂-TiO₂-IrO₂三种析氯阳极进行性能对比。通过SEM、EDS、XRD等方法表征测试阳极表面形貌、元素及组成,考察了氯化钠浓度、电流密度、停开频率对阳极析氯效果和寿命的影响。研究发现,Ti/RuO₂-IrO₂-SnO₂-Sb₂O₅阳极活性强、稳定性高;阳极涂层各组分高度融合为固溶体,结构致密,稳定性强;在15 g·L^-1 NaCl、400 A·m^-2电流密度、20℃条件下,Ti/RuO₂-IrO₂-SnO₂-Sb₂O₅阳极电解的电流效率达到91.55%;频繁停开、强化电解条件下寿命达到231 h,是Ti/RuO₂-TiO₂阳极的77倍,预估在400 A·m^-2电流密度下能够使用20年。     

Ti基IrO2＋Ta2O5阳极在H2SO4溶液中的电解时效行为

研究了450 ℃制备所得Ti/70％IrO2 30％Ta2O5（摩尔分数）高寿命阳极在H2SO4溶液电解过程中电极的物理、化学及电化学性能的时效行为.结果发现，整个电解过程可分为“活化”、“稳定”及“失效”三个阶段.在“活化”及“稳定”区内主要发生电极表面活性氧化物的溶解，涂层中IrO2金红石相的（110）、（101）晶面择优取向随电解时间延长而减弱，而（002）晶面择优增强.但是在“失效区”内，各晶面的择优程度却不随电解时间的变化而变化，这表明在“失效区”内氧化物的损失机制发生了变化.电化学阻抗谱测试表明，电极的析氧电化学反应电阻随电解时间的延长发生缓慢而连续的上升，而整个电极的物理阻抗在“失效区”内却发生突升现象.X射线衍射分析（XRD）表明，随电解时间的延长TiO2金红石相的衍射强度增大，达“失效区”时衍射强度发生突升.根据实验现象特别是“失效区”内阳极的时效行为提出高寿命Ti基氧化物涂层阳极的失效机制.     

刻蚀剂对IrO_2-MnO_2阳极纳米涂层表面形貌及电化学行为的影响

采用传统热分解法制得了不同刻蚀剂(HCl、H2SO4、C2H2O4和HF)处理的Ti基Ir O2-Mn O2纳米涂层阳极,使用场发射扫描电子显微镜(FESEM)、循环伏安(CV)及极化技术等观察和研究各纳米涂层阳极表面形貌及其电化学性能.结果表明,与HCl和C2H2O4刻蚀剂相比,HF和H2SO4刻蚀的基底涂层表面Ir O2纳米颗粒更为密集且尺寸更大;H2SO4刻蚀处理的Ti基Ir O2-Mn O2阳极电催化活性最佳,HF次之,C2H2O4再次之,HCl最差.     

F-和Fe3+掺杂对Ti基PbO2阳极性能的影响

采用热分解-电镀法制备了Ti基PbO2,阳极(Ti/PbO2),F-掺杂PbO2阳极(Ti/F-PbO2),Fe3+掺杂PbO2阳极(TiP/Fe-PbO2)和F-,Fe3+共掺杂PbO2,阳极(Ti/F-Fe-PbO2).采用XRD和EDX测试对电极进行了表征,应用加速电解寿命测试和电催化降解4-氯苯酚(4-CP)污水,考察了F-掺杂,Fe3+掺杂和F-,Fe3+共掺杂对PbO2阳极稳定性及电催化活性的影响.结果表明,Ti/F-PbO2和Ti/FePbO2阳极有相近的电催化降解活性,但与Fe3+掺杂相比,F-掺杂大大提高了PbO2阳极的加速电解寿命.对Ti/F-Fe-PbO2阳极,Fe3+掺杂改善了其导电性能.同时F-掺杂提高了阳极的稳定性能,使其有较长的电解寿命.与Ti/PbO2,Ti/F-PbO2和Ti/Fe-PbO2阳极相比,Ti/F-Fe-PbO2阳极的电催化降解活性显著提高,这不仅与其导电性能的改善有关,更与F-掺杂和Fe3+掺杂对4-CP降解的表面协同作用有关.     

钌-钯掺杂Ti/TiO2阳极电催化降解甲基橙研究

以偶氮染料甲基橙为处理对象, 分别考察了Ru, Pd及Ru-Pd掺杂的Ti/TiO2阳极的光、电催化活性, 并与Ti/RuOx-PdO阳极的电催化活性进行了比较; 利用XPS分析了Ru-Pd掺杂的Ti/TiO2阳极表面Ru, Pd及Ti的化学形态. 实验发现, Ru, Pd及Ru-Pd掺杂的Ti/TiO2阳极的光催化活性都有所降低, 而其电催化活性却都有大幅提升, 特别是Ru-Pd掺杂的Ti/TiO2阳极, 其电催化活性明显地优于Ti/RuOx-PdO阳极. XPS分析表明, Ru-Pd掺杂的Ti/TiO2阳极其光、电催化活性的变化可能与该阳极表面Ru, Pd及Ti的化学形态变化有关.     

Ir0.08Ti0.92O2及其载Pt催化剂的制备与电催化性能

采用TiN浸渍热分解法制备了低铱含量Ir0.08Ti0.92O2纳米粉体,再通过微波辅助制备Pt/Ir0.08Ti0.92O2催化剂,并与采用传统亚当斯法制备的IrO2和商品化Pt/C进行对比研究.利用X射线衍射(XRD)、透射电子显微镜(SEM)、X射线能量散射谱(EDS)和X射线光电子能谱(XPS)对产物进行了分析.结果表明,Ir0.08Ti0.92O2是一种纳米棒状金红石相固溶体,直径约15 nm,担载Pt粒度5~7 nm,其中本体Ir/Ti原子比为0.084∶0.916,表面Ir/Ti原子比为0.296∶0.704,表明Ir在表面发生富集.经稳态极化曲线和线性扫描伏安测试得到析氧反应的本征催化活性由高到低为Ir0.08Ti0.92O2>Pt/Ir0.08Ti0.92O2>IrO2,前两者性能相近;Pt/Ir0.08Ti0.92O2的氧还原反应活性低于Pt/C,需进一步优化载Pt粒度.研究结果表明,Ir0.08Ti0.92O2既是高效、低成本的析氧反应催化剂,也是高性能载体材料,这使Pt/Ir0.08Ti0.92O2作为双效催化剂在成本、催化性能和稳定性上具有更大优势,也可作为优异的析氢反应催化剂.     

不同掺杂元素的钛基PbO2电极对苯酚电催化氧化性能的影响

本文在SnO2-Sb2O5氧化物为中间层的钛基体上,采用电沉积法制备了无掺杂的Ti/PbO2、掺杂F的Ti/PbO2(Ti/PbO2+F)和掺杂Co3O4纳米粒子的Ti/PbO2电极(Ti/PbO2+Nano-Co3O4).用X射线衍射(XRD)和扫描电镜(SEM)分析和观察了电极材料的组成、结构和形貌,并通过电化学方法研究了这三种电极对苯酚的电催化氧化性能.结果表明,Ti/PbO2+F电极的析氧电位较Ti/PbO2电极的发生明显正移,但其苯酚的氧化峰和析氧峰并不能分开;而Ti/PbO2+Nano-Co3O4电极虽然其析氧电位负移,但对苯酚的氧化峰出现在析氧峰之前.这一结果表明,体系存在着某种反应特别快的瞬态中间体,即在水分子被解离之前已与苯酚发生了反应,从而更有利于苯酚的转化和降解.     

低温海水用钛基金属氧化物阳极的制备与性能

将Ti N纳米粉体与Ta Cl5正丁醇饱和溶液混合制得中间层涂覆液,通过热分解法在不同焙烧温度下得到了含有中间层的Ti/(Ti-Tax)O2/Ir O2电极,并与相同工艺下得到的传统Ti/Ir O2电极进行对比分析.采用X射线衍射和扫描电子显微镜对制备的电极进行了表征,通过循环伏安曲线、极化曲线和恒流加速寿命测试等电化学手段对电极性能进行了分析.结果表明,引入中间层可以使Ti/(Ti-Tax)O2/Ir O2电极400℃低温焙烧样品表层Ir O2结晶发育更好,得到了通常高温下才具有的典型龟裂纹形貌;相对于500℃高温焙烧样品,其在海水中的电化学活性表面积提高近6倍,在4℃和100 m A/cm2电流密度下的电极电位(1.37 V)降低100 m V,催化性能得到显著提高;同时加速寿命相对于传统的Ti/Ir O2电极提高10倍以上,是一种适用于低温海水环境的、具有较高活性和耐久性的新型阳极.     

析氯钛基RuO_2－Co_3O_4－TiO_2（60）涂层的研究

用稳定极化、Ｘ射线衍射、透射电镜和扫描电镜的方法研究了钛基ＲｕＯ_２－Ｃｏ_３Ｏ_４－ＴｉＯ_２（６０）涂层的析氯活性、导电性、使用寿命、微观结构和表面形貌。并对其活性表面积进行了评价。详细讨论了涂层成份、微观结构和表面形貌对涂层析氯活性和活性表面积的影响。发现在０～１０ｍ／ｏＣｏ_３Ｏ_４和６０ｍ／ｏＴｉＯ_２成份范围内ＲｕＯ_２、Ｃｏ_３Ｏ_４和ＴｉＯ_２可形成单一金红石型固溶体,且有优异的析氯活性、电导率和使用寿命。以此研究为基础可改进氯碱工业广泛使用的传统ＲｕＯ_２－ＴｉＯ_２阳极,降低阳极涂层中贵金属含量,提高阳极的电化学性能．     

Ir/CeO2催化剂的表征和CO氧化性能

采用浸渍法制备了Ir/CeO2催化剂,考察了催化剂的CO氧化活性。随着Ir负载量的增加,Ir/CeO2催化剂的CO氧化活性先上升后下降,当Ir的负载量为1%时,催化剂的活性最高。Ir/CeO2催化剂中Ir以IrO2的形式存在,当低负载量(≤1%)时以高分散形式存在;高负载量(>1%)时以晶相IrO2的形式存在。随着Ir负载量增加,Ir粒子逐渐变大,反应比速率和反应转换频率(TOF)逐渐下降,表明小粒子上具有更高的CO反应活性。同时也发现金属态Ir催化剂的CO氧化活性高于氧化态IrOx催化剂。     

Titanium Anodes with Active Coatings Based on Iridium Oxides: The Chemical Composition of the Coatings and the Distribution of Their Components over Depth on Anodes Made of IrO2, IrO2 + TiO2, IrO2 + RuO2 + TiO2, and IrO2 + RuO2 + TiO2 + Ta2O5

The distribution of components of active coatings over depth and the valence of metals that constitute the coatings on the IrO₂, IrO₂ + TiO₂, IrO₂ + RuO₂ + TiO₂, and IrO₂ + RuO₂ + TiO₂ + Ta₂O₅ anodes are established using Auger electron spectroscopy and x-ray photoelectron spectroscopy. It is shown that all metals, with the exception of tantalum, exist in a coating in a tetravalent state, in the form of relevant dioxides. Tantalum is present in the coatings in the form of Ta₂O₅. Etching the coatings with the argon and neon ions leads to the reduction of iridium and ruthenium dioxides to relevant metals and a partial reduction of TiO₂ to TiO. It follows that the x-ray photoelectron spectroscopy method allows one to determine the valence of metals that make up a coating only in the surface layers of the coatings. It is shown that for all the anodes, with the exception of anodes containing Ta₂O₅, the composition of a coating barely alters with depth and satisfactorily conforms to the composition specified by the coating formula. For the anodes whose coating is containing Ta₂O₅ there is observed high enrichment of surface layers of the coating by iridium and tantalum. This is probably explained by the system's multiphaseness and by a substantial difference in the temperatures at which the formation of relevant phases occurs in the course of pyrolysis.     

Titanium Anodes with an Active Coating Based on Iridium Oxides: The Effect of the Coating's Thickness,Porosity, and Morphology on Its Stability,Selectivity, and Catalytic Activity

The corrosion resistance and the electrochemical behavior of oxide iridium-ruthenium titanium anode (OIRTA) containing 4 mol % RuO₂ + 26 mol % IrO₂ + 70 mol % TiO₂, with a relatively thick active coating (iridium load 15 g m^?2) are studied in conditions of chlorine electrolysis. It is established that polarization curves for the chlorine evolution at low currents exhibit an extended “Tafel” segment with a “Nernstian” slope equal to 0.036 V and that the process rate is limited by the chlorine diffusion away from the electrode surface. In the region of high currents, which is precisely where the chlorine evolution reaction is realized in the industry, polarization curves start displaying an extended, practically horizontal, segment of low polarizability (SOLP) and the chlorine evolution occurs out of the entire depth of the coating. It is shown that the rate of iridium dissolution out of these anodes is in excess of the rate of its dissolution out of OIRTA with a thin coating and the larger the iridium load in the coating, the larger the excess. This phenomenon is attributed to a higher porosity of OIRTA with a thick coating and to the occurrence of the process of iridium dissolution out of the coating throughout the entire depth of the coating. As a result, such an increase in the coating's thickness is likely to lead to a decrease in the lifetime of the anodes. It is discovered that a prolonged polarization of OIRTA in the region of the SOLP leads to an increase in the overvoltage and to a practically complete disappearance of the SOLP from the polarization curves. All this served as the grounds for our drawing the conclusion that it would make no sense to enlarge the thickness and increase the porosity of the active coating of the OIRTA anodes in order to enhance their catalytic activity. It proved manageable to produce substantially more efficient anodes by depositing a thin active coating onto rough titanium out of a diluted covering solution. In so doing, the OIRTA anodes possessed a higher corrosion resistance and a better selectivity at a small iridium load in the coating.     

Effect of the iridium oxide thin film on the electrochemical activity of platinum nanoparticles

The influence of the iridium oxide thin film on the electrocatalytic properties of platinum nanoparticles was investigated using the electro-oxidation of methanol and CO as a probe. The presence of the IrO(2) thin film leads to the homogeneous dispersion of Pt nanoparticles. For comparison, polycrystalline platinum and Pt nanoparticles dispersed on a Ti substrate in the absence of an IrO(2) layer (Ti/Pt) were also investigated in this study. Inverted and enhanced CO bipolar peaks were observed using an in situ electrochemical Fourier transform infrared technique during the methanol oxidation on the Pt nanoparticles dispersed on a Ti substrate. Electrochemical impedance studies showed that the charge transfer resistance was significantly lower for the Ti/IrO(2)/Pt electrode compared with that of the massive Pt and Ti/Pt nanoparticles. The presence of the IrO(2) thin film not only greatly increases the active surface area but also promotes CO oxidation at a much lower electrode potential, thus, significantly enhancing the electrocatalytic activity of Pt nanoparticles toward methanol electro-oxidation.     

Effects of synthesis conditions on the electrochemical activity of titanium anodes with iridium oxide coating

The effects of temperature, heat treatment time, and iridium content in the active layer on the electrocatalytic activity of titanium anodes with active coating during oxygen evolution in 0.5 M sulfuric acid have been investigated. The highest activity of these electrodes is reached when the temperature of final treatment is 450°C, treatment time is 25 min, and iridium content in the active layer is over 2 g/cm². An X-ray photoelectron spectroscopy study showed that iridium is predominantly in the tetravalent oxidized state in the active layer.     

钛基氧化物Ru_((0.4-x))Ir_xTi_(0.6)电极电化学性能研究

应用热分解法制备Ru(0.4-x)IrxTi0.6三元金属氧化物电极,研究IrO2含量对电极析氯性能、催化选择性、强化寿命以及表面形貌的影响.结果表明:IrO2的加入使涂层的抗析氧腐蚀能力增强,膜电阻和反应电阻降低,强化寿命随着IrO2含量的增加而增长,由原来的1.0h提高到97h;IrO2含量为10%时,析氯电位低、析氧电位高、催化选择性好.一定量的IrO2的加入有利于细化晶粒、粗化表面.     

有机碳源对LiTi2(PO4)3/C复合水系负极性能的影响

采用喷雾干燥与高温煅烧相结合的方法制备了球形LiTi₂(PO₄)₃/C复合水系负极材料, 探讨了基于不同包覆机制的有机碳源和碳包覆量对LiTi₂(PO₄)₃/C复合负极电化学性能的影响. 结果表明, 碳包覆量过低时不足以阻止水的侵蚀, 而碳含量过高时锂离子扩散的阻力过大, 磷酸钛锂电极最优碳包覆质量分数为13%. 碳包覆的均匀性和包覆层厚度是影响电极性能的两个重要因素. 基于原位聚合包覆机制的聚多巴胺包覆磷酸钛锂颗粒最均匀, 碳化后微晶结构较好, 具有良好的电子导电性, 以聚多巴胺为碳源制备的LiTi₂(PO₄)₃/C复合负极性能最优.